Process for enzymatic hydrolysis of lignocellulosic material and fermentation of sugars
The invention relates to a process for the preparation of a sugar product from lignocellulosic material, comprising the following steps: a) optionally pre-treatment of the ligno-cellulosic material; b) optionally washing of the optionally pre-treated ligno-cellulosic material; c) enzymatic hydrolysis of the optionally washed and/or optionally pre-treated ligno-cellulosic material using an enzyme composition comprising at least two cellulase and whereby the enzyme composition at least comprises GH61; and d) optionally recovery of a sugar product; wherein during part of the time of the enzymatic hydrolysis, oxygen is added to the ligno-cellulosic material and during part of the time of the enzymatic hydrolysis less oxygen is added to the ligno-cellulosic material compared to the other part of the time of the enzymatic hydrolysis, preferably no oxygen is added to the ligno-cellulosic material.
1. A process for preparation of a sugar product from lignocellulosic material, comprising:
enzymatic hydrolysis of the lignocellulosic material using an enzyme composition comprising at least two cellulases and whereby the enzyme composition at least comprises GH61; and
wherein:
the enzymatic hydrolysis occurs for a first part of time and a subsequent second part of time;
during the first part of time dissolved oxygen concentration in the lignocellulosic material is less than the dissolved oxygen concentration during the second part of time, during the second part of time oxygen is added to the lignocellulosic material, and the second part of time is 2% to 80% of total enzymatic hydrolysis time.
2. A process for preparation of a fermentation product from lignocellulosic material, comprising:
enzymatic hydrolysis of the lignocellulosic material using an enzyme composition comprising at least two cellulases and whereby the enzyme composition at least comprises GH61;
fermentation of the hydrolysed lignocellulosic material to produce a fermentation product
wherein:
the enzymatic hydrolysis occurs for a first part of time and a subsequent second part of time;
during the first part of time dissolved oxygen concentration in the lignocellulosic material is less than the dissolved oxygen concentration during the second part of time, during the second part of time oxygen is added to the lignocellulosic material, and the second part of time is 2% to 80% of total enzymatic hydrolysis time.
3. The process according to claim 1 , wherein the second part of the time is added is 10 to 80% of the total enzymatic hydrolysis time.
4. The process according to claim 1 whereby the dissolved oxygen concentration during the second part of the time is at least 2 times the dissolved oxygen concentration during the first part of the time.
5. The process according to claim 1 , wherein the oxygen is added in the form of bubbles.
6. The process according to claim 1 , wherein the enzymatic hydrolysis takes place in a reactor having a volume of 1 m 3 or more.
7. The process according to claim 1 , wherein the total enzymatic hydrolysis time is 5 to 150 hours.
8. The process according to claim 1 , wherein the enzyme composition used retains activity for 30 hours or more.
9. The process according to claim 1 , wherein the enzymatic hydrolysis is conducted at a temperature of 45° C. or more.
10. The process according to claim 1 , wherein the enzyme composition is from a fungus, or the enzyme composition comprises a fungal enzyme.
11. The process according to claim 1 , wherein dry matter content in the enzymatic hydrolysis is 10 wt % or more.
12. The process according to claim 1 in which the enzymatic hydrolysis takes place in a batch, fed batch and/or continuous culture reactor.
13. The process according to claim 1 in which oxygen is introduced as air.
14. The process according to claim 10 , wherein the fungus is of the genus Rasamsonia, or the fungal enzyme is a Rasamsonia enzyme.
15. The process according to claim 1 , wherein during the first part of time dissolved oxygen in the lignocellulosic material is at a concentration that is at least 50% less than during the second part of time, and during the second part of time oxygen is added to the lignocellulosic material continuously.
16. The process according to claim 1 , wherein the second part of time is 12% to 50% of total enzymatic hydrolysis time.
17. The process according to claim 1 , wherein dry matter content in the enzymatic hydrolysis is 14 to 33% wt %.
18. The process according to claim 1 , wherein, the dissolved oxygen concentration is maintained in the range of 0.02 mol/m 3 to 0.045 mol/m 3 , and wherein dissolved oxygen is measured under normal atmospheric pressure and at about 62° C.